CN102753251B - Utilize plasma-pump and the oxygen separation method of film and system - Google Patents
Utilize plasma-pump and the oxygen separation method of film and system Download PDFInfo
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- CN102753251B CN102753251B CN201080056788.8A CN201080056788A CN102753251B CN 102753251 B CN102753251 B CN 102753251B CN 201080056788 A CN201080056788 A CN 201080056788A CN 102753251 B CN102753251 B CN 102753251B
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- oxygen
- gas
- pump
- plasma
- inoranic membrane
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
- A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
- A61M16/10—Preparation of respiratory gases or vapours
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
- A61M16/00—Devices for influencing the respiratory system of patients by gas treatment, e.g. mouth-to-mouth respiration; Tracheal tubes
- A61M16/10—Preparation of respiratory gases or vapours
- A61M16/1005—Preparation of respiratory gases or vapours with O2 features or with parameter measurement
- A61M16/101—Preparation of respiratory gases or vapours with O2 features or with parameter measurement using an oxygen concentrator
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
- B01D53/323—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00 by electrostatic effects or by high-voltage electric fields
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0229—Purification or separation processes
- C01B13/0248—Physical processing only
- C01B13/0251—Physical processing only by making use of membranes
- C01B13/0255—Physical processing only by making use of membranes characterised by the type of membrane
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
- A61M2205/00—General characteristics of the apparatus
- A61M2205/36—General characteristics of the apparatus related to heating or cooling
- A61M2205/3606—General characteristics of the apparatus related to heating or cooling cooled
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/12—Oxygen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/10—Single element gases other than halogens
- B01D2257/104—Oxygen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/45—Gas separation or purification devices adapted for specific applications
- B01D2259/4533—Gas separation or purification devices adapted for specific applications for medical purposes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0046—Nitrogen
Abstract
The present invention relates to a kind of method for separating oxygen from the gas comprise oxygen, described method comprises the steps: the gas compressing in plasma-pump (16) and comprising oxygen described in heating, heated and compression the gas comprising oxygen is guided the major opposing side to compact inorganic film (58), thus by the described gas comprising oxygen, described inoranic membrane is heated to the permeable temperature of oxygen, and between the major opposing side and secondary side of described inoranic membrane (58), produce pressure differential, wherein, create the oxygen stream through described inoranic membrane (58), from the described gas comprising oxygen, thus separate oxygen.
Description
Technical field
The present invention relates to the field of oxygen separation.More particularly the invention relate to treatment use
Oxygen separation, especially at home care areas.
Background technology
Oxygen therapy is to bestow oxygen as Therapeutic mode.Because oxygen is the key of cell metabolism,
And tissue oxidizing effect is the key of all physiological functions then, oxygen therapy for various purposes by
It is widely used in during chronic and acute patient nurses.Oxygen therapy should be used by increasing the oxygen to lung
Gas supply also thus increases the available quantity of the oxygen to bodily tissue to make patient benefit, and is especially suffering from
Person stand histanoxia and/or blood oxygen too low time.Oxygen therapy can be used for hospital or home care two
In the application of person.The main home care application of oxygen therapy is for suffering from severe chronic obstructive pulmonary
The patient of sick (COPD).
Oxygen can be bestowed by several mode.That oxygen is bestowed it is preferable that so-called oxygen
On-demand generation.Thus, business industry & solution, the most so-called oxygen concentrator or separation
Device, is well-known.These oxygen concentrators separate oxygen mostly from the gas comprising oxygen,
Thus as required, the most directly provide oxygen.Most known oxygen concentrators need
Compressor is with the oxygenous gas of compressed package.Further, it is necessary to generation oxygen, preferably pure oxygen.Most
Therefore known oxygen concentrator includes for the organic membrane from the gas separation oxygen comprising oxygen.
The major defect of known oxygen concentrator is high cost and convenience limited for noise.
Additionally, comprise undesirable component of the gas of oxygen, mainly nitrogen, film is absorbed, by
This causes the essential condition of so-called rocking process (swing process), by this process, is absorbed
Gas disengage from film.During desorption procedure, it is impossible to separate oxygen, thus, it is desirable to have two
Individual film, and this can increase cost further.In addition, described compressor has noise mostly,
Convenience is caused to reduce, especially when using this oxygen concentrator whole night.Additionally, the oxygen generated
Gas is non-sterile, and therefore, further disinfectant measure may often be such that desired or necessary.
Conventional oxygen concentrator is huge, heavy and needs patient and caregivers to carry out day
Often safeguard.Such device produces noise and heat.Further, it is desirable to reduce the one-tenth of regular purchase cost
The cost price (contribution of compressor unit is notable) of this price and service.
Definition
Term " dense film ", as used herein, it should refer to oxygen can be passed through but to other
Gas (especially to nitrogen) impervious film.
Term " comprises the gas of oxygen ", as used herein, it should refer at least partly include
Any gas of oxygen.
" major opposing side " of term film, as used herein, it should refer to film leads to plasma-pump
Side.
" the secondary side " of term film, as used herein, it should refer to that the film unit that leads to of film goes out
The side of mouth.
Summary of the invention
It is an object of the invention to provide a kind of method separating oxygen, its cost-effective and improve about
Safeguard and the convenience of noise.
This purpose can be realized by the method separating oxygen from the gas comprise oxygen, described
Method comprises the steps: to be compressed, in plasma-pump, the gas comprising oxygen and heat, will
Heated and compression the gas comprising oxygen guides the major opposing side to compact inorganic film, from there through bag
Described inoranic membrane is heated to the permeable temperature of oxygen, and the master at inoranic membrane by oxygenous gas
Produce pressure differential between side and secondary side, wherein, produce through the oxygen stream of inoranic membrane, thus from
Comprise separation oxygen in the gas of oxygen.
The present invention is based on beyond thought discovery, i.e. in plasma-pump, heating and compressed package are oxygenous
Gas separate with by inoranic membrane the combination of oxygen result in wondrous and be highly profitable collaborative
Effect.
By using plasma-pump, compress in one step and heat the gas comprising oxygen.This leads
Caused such advantage, the most so without requiring for heat compressed gas extra equipment or
Film.On the contrary, the gas leaving plasma-pump has sufficiently high temperature to heat inoranic membrane, thus real
Show the sufficiently high oxygen stream by described film.Therefore, by utilizing plasma-pump compressed gas,
The compressed gas comprising oxygen has the temperature of rising, and this effect being generally not desirable to it is possible to
Very well with inoranic membrane combination application.
Additionally, in the case of plasma-pump operates in noise decrease, it is achieved that the raising of convenience, especially
It is in home care is applied.By providing the plasma for heating the gas oxygenous with compressed package
Pump, the device used has size and the weight of minimizing especially advantageous for home care is applied,
Convenience has obtained further improvement.
It addition, had the device of plasma-pump and inoranic membrane by use, due to such device
Can be designed the most cheap, it is achieved that with relatively low cost separation oxygen, and additionally, with existing
There is known method in technology to compare, improve energy efficiency.
Another advantage of the method according to the invention is the generation of aseptic oxygen.Extra sterilization and aseptic
It is unnecessary for changing step.According to the present invention, it is provided that the on-demand generation of aseptic oxygen.
It addition, rocking process is no longer necessary, because nitrogen is not absorbed by inoranic membrane, the most right
Being construed as limiting through condition of oxygen.
By utilizing plasma-pump to substitute known compressor from the prior art, it is possible to achieve cost price
The increase of lattice, service and noise.
In a preferred embodiment of the invention, air is used as comprising the gas of oxygen.This protects in family
Ought to in especially preferably as the special gas comprising oxygen need not be stored.
In another embodiment, the gas compression scope to >=2.5 bars of oxygen will be comprised, with in secondary side
The oxygen pressure of superatmospheric is directly obtained on face.This pressure may be enough to make sufficiently high oxygen
Stream passes through inoranic membrane, it is provided that the sufficient stream of the pure oxygen generated.Thus, if will bag
Oxygenous gas compression is to the scope of 5 bars, and this is advantageous particularly.
In another embodiment, the gas comprising oxygen is heated to >=900K and≤1300K
Temperature range.By the gas comprising oxygen that offer is the most heated, inoranic membrane is heated to foot
Enough high temperature are to provide the sufficient transmitance character for oxygen.
In another embodiment, after releasing oxygen is cooled down.This achieves the oxygen to patient
Directly bestowing of gas.Therefore the amount of cooling may adapt to specifically use.In some applications, uncommon
Hope and oxygen is cooled to room temperature, and when using when relative to oxygen at the upborne temperature of room temperature,
Some application are more efficiently.
Can be by realizing the method according to the invention, described dress according to the gas fractionation unit of the present invention
Put the plasma-pump included for compressing and heat the gas comprising oxygen, and there is compact inorganic film
Film unit, wherein, described plasma-pump and film unit connect via pipeline, and described pipeline is designed
Become and will guide to film unit from the gas comprising oxygen of the heated of plasma-pump and compression, and
Described compact inorganic film is designed to from the gas comprising oxygen separate oxygen.
In one embodiment, inoranic membrane is formed with tubular form.This achieves highly stable geometry
Structure and can also allow for being formed the film unit of the size with reduction.
In another embodiment, described device includes the cooler being disposed in the downstream of described film unit.
Described cooler makes generated oxygen can be cooled to be suitable to directly bestow to the temperature of patient.
In another embodiment, pneumatic reservoir provides in the downstream of described plasma-pump.This achieves
Comprise the gas of oxygen and the formation of the therefore continuously stream of pure oxygen.
In another embodiment, inoranic membrane is fixed to be formed as the supporter of perforated membrane.This achieves
Highly stable structure, it is not necessary to form more stable such oxygen selective membrane, it reduce into
This.
In another embodiment, the outside offer at inner shell is thermally isolated.This achieves more preferable heat
Efficiency also reduces required energy input, thus reduces cost.In this article, if be thermally isolated
Being designed to vacuum, this is especially preferred.This is to produce to be thermally isolated to be particularly easy to and effective side
Formula.
Accompanying drawing explanation
According to embodiments described just below, these and other aspects of the present invention will become clear from also
Illustrated.
In the accompanying drawings:
Fig. 1 shows the schematic block diagram of the operation principle of the method according to the invention；
Fig. 2 shows the diagrammatic cross-sectional view of the plasma-pump according to the present invention；
Fig. 3 shows the diagrammatic cross-sectional view of the film unit according to the present invention.
Detailed description of the invention
In FIG, the device 10 for separating oxygen from the gas comprise oxygen is diagrammatically illustrated.
The oxygen therapy that device 10 is very suitable for such as in home care is applied.But, according to the present invention's
Device 10 and method are not limited to treatment use, but the oxygen being further adapted for all kinds generates.Make
For another example use, with reference to the oxygen in aircraft and generate.
Device 10 includes that the gas for comprising oxygen guides to the gas access 12 arranged in 10.
The gas comprising oxygen is guided to be entered in plasma-pump 16 by gas access 12, and below
In, gas enters the film unit 22 for separating oxygen by pipeline 18.In the downstream of film unit 22,
The pure oxygen generated can be guided to cooler 26 by pipeline 24, carries in the downstream of described cooler
For the outlet 28 for bestowing oxygen.Describe device 10 in further detail below.
The gas comprising oxygen is guided the gas discharge (discharge) to algorithm for power modulation by gas access 12
Compression unit, i.e. plasma-pump 16.Show in further detail Exemplary plasma pump 16 in fig. 2,
It is highly suitable for the method according to the invention.
Plasma-pump 16 can include the arc chamber 30 with gas discharge device 32, in electric discharge
Room 30 is internally generated gas discharge.Gas discharge device 32 can include by capacitive character, inductive,
Surface wave and/or microwave coupling generate the coupling device of gas discharge, and carry for described coupling device
Energy source 34 for alternating current.Described coupling device can include two electrodes 36,38, described electricity
Pole is disposed in the outside of gas discharge chamber 30, and for capacitive couplings, and described electrode can be by
Carbon is formed.Preferably, coupling device is disposed in the outside of gas discharge chamber 30.Coupling device is especially
It is that the abrasion of the parts of electrode 36,38 can be significantly reduced.But, it is also possible to by coupling device
Parts are at least partially disposed at the inside of arc chamber.Utilize energy source 34, it is possible to apply the voltage to
Between two electrodes 36,38, cause the isoionic generation within gas discharge and arc chamber 30.
Alternating current allows to maintain over time plasma, by changing the amplitude of alternating current, it is possible to modulation
Isoionic power.
Arc chamber 30 also includes gas access the 40, first gas outlet 42 and the second gas outlet 44.
The gas access 40 of plasma-pump 16 is connected to the gas access 12 of device 10.First gas outlet
42 can also include tapping equipment 46, and it can be designed as simple two-way valve.Described two-way valve exists
Side is connected to arc chamber 30, and is connected to air or for discharging the storage of gas at opposite side
Device.
Arc chamber 30 is further attached to the second gas outlet 44, and it is connected to pipeline 18 then.For
Controlling by gas access 40 and the gas stream of the second gas outlet 44, inlet valve 48 enters with gas
Mouth 40 connects and outlet valve 50 is connected (seeing Fig. 1) with the second gas outlet 44.For example, it is possible to
Use check-valves or two-way valve as inlet valve 48 and outlet valve 50.Check-valves is preferred as them
It is made without controlling.By making the operation adaptation of inlet valve 48 and outlet valve 50 through algorithm for power modulation
Gas discharge, it is possible to generate the gas stream with specific direction.
By generating plasma in arc chamber 30 as described above, generate and pressurized comprise oxygen
The gas of gas.During isoionic high power operation, the pressure in arc chamber 30 can increase, and
During low-power operation or closedown plasma, described pressure can reduce.By in arc chamber 30
Run the electric discharge through algorithm for power modulation and be obtained in that pressure-swing.
Hereinafter, by the operation with exemplary mode plasma-pump described in more detail 16.
In the first step, near atmospheric, such as 1 bar, and approximating room temperature, such as 300
K, starts with tapping equipment 46, inlet valve 48 and the outlet valve 50 closed.Generate and maintain electric discharge
The high power plasma of chamber interior, to obtain the rising of temperature.Owing to arc chamber is isolated with surrounding air,
The gas comprising oxygen in the arc chamber of plasma-pump 16 is compressed.Exemplarily, due to by wait from
Son causes the temperature of gas to be increased to the temperature of up to 900K, and therefore described pressure may be added to 3
The value of bar.By opening outlet valve 50, the gas comprising oxygen in arc chamber 30 is only capable of by stream
Enter pipeline 18 and leave room 30, thus in arc chamber 30, reach the further liter of 2100K scope
Constant pressure is caused at a temperature of height.After specific interval, in third step, gas discharges
Device 46 can be opened to surrounding air.During this stage, the pressure in arc chamber 30 drops to
Atmospheric pressure and temperature are added to the temperature of about 1550K.After specific interval, discharge power
It is significantly reduced or is switched to cause gas temperature to fall to approximately room temperature, such as 300K.Fresh
The gas comprising oxygen at this moment can be flowed in arc chamber 30 by gas access 12 and entrance 40.
After another time interval, complete circulation.If proceeded, plasma-pump 16 again with
First step starts.If plasma is not switched off, it is possible to save light in the next step etc. from
Son.
Can not overlapping with corresponding step in the case of operate plasma-pump 16.Or, it is possible to use
Overlapping one or more steps operates plasma-pump 16.
As described above, during burning plasma, gas temperature may be the highest.Despite the presence of leading
The wall causing plasma-pump 16 has the Temperature Distribution of the temperature reduced relative to central shaft, but uses such as stone
The temperature stable materia of English glass or aluminum oxide is favourable as the wall material of plasma-pump.
Typically for plasma-pump 16, fairly small energy input is enough.Specifically, root
According to temperature and membranaceous condition, the power input of 100W to 300W is probably enough.This power is defeated
The scope entered is very suitable for home care application.
Energy source 34 can deliver the square wave current I of the 300Hz frequency of the output with change,
Can be so that electric current IAveragelyIn root-mean-square (rms) value of 300Hz driving frequency more than t=50ms's
Change in time scale.For electronic driver, the electric current I of several amperesAveragelySum hectowatt
Power is feasible.Energy source 10 delivers the crest voltage of up to 20kV to obtain also for the incipient stage
Obtain gas and decompose/light plasma.
Working in described circulation, plasma-pump 16 is used as gas pump.Although plasma-pump 16
Working in different circulations, due to the altofrequency of cycle of operation, it can generate the gas comprising oxygen
Direct and the continuous print stream of body.
In order to support continuous print stream further, preferably provide pneumatic reservoir in the downstream of outlet valve 50
52.By the gas comprising oxygen being pressed onto the inside of pneumatic reservoir 52, preferably from arc chamber 30
Reservoir valve 54 is provided by utilizing or alternatively provides throttle orifice to increase the stream in pneumatic reservoir downstream
Resistance, it is possible to generate the excess pressure within reservoir 52.Constant or nearly constant excess pressure can be used
In the continuous or subcontinuous stream generating the gas comprising oxygen in pipeline 18.
In the downstream of plasma-pump 16 or reservoir 52, the described gas comprising oxygen is guided extremely respectively
Film unit 22.Upstream at film unit 22, it is provided that valve, described valve can be reservoir valve 54
Or extra valve.When comprising the insufficient pressure of gas of oxygen, this valve can blind off a line 18.
On the contrary, when having reached sufficiently high pressure, described valve can open pipeline 18.Therefore, it can
Thering is provided, under the pressure of >=2.5 bars, the most under a pressure of 5 bars, valve is opened, and thus will bag
Oxygenous gas guides to film unit 22.
Fig. 3 shows the cross sectional view of film unit 22.Film unit 22 can have any configuration.So
And, the tubular form of film unit 22 is especially advantageous.Therein, film unit 22 includes internal duct
56, it is connected with pipeline 18 fluid and allows to comprise the gas entrance film unit 22 of oxygen.Internal duct
56 are limited by inoranic membrane 58 outside it, and inoranic membrane 58 has major opposing side and time side.Described master
Face is led to internal duct 56 and thereby opens into plasma-pump 16, and exterior line 60 is led in secondary side.
Exterior line 60 side therein is limited by inoranic membrane 58, and in its exterior lateral sides by inner shell
Body 62 limits.Inner shell 62 can be by high temperature resistance material (such as quartz glass or pottery alumina
Compound) pipe made.The purpose of exterior line 60 is that separated oxygen is derived film unit 22 also
Therefore it is connected with pipeline 24 fluid.Outside at inner shell 60, it is provided that be thermally isolated 64.This heat
Isolation can be preferably the vacuum provided between inner shell 62 and external shell 66.Can also be
Noble gas is provided between inner shell 62 and external shell 66.In such a situation it is preferred to it is permissible
There is provided the shortest distance to realize enough isolation between inner shell 62 and external shell 66.
But, described isolation 64 can be enough to obtain from any kind of isolation known in the art
Isolation effect.External shell 66 can be designed as such as based on aluminum heat shielding, to improve further
Isolation.This actually improves the energy efficiency of device 10 and thereby saving cost.
Referring back to inoranic membrane 58, its objective is that the stream from remaining delay (i.e. comprises the gas of oxygen
Remaining ingredient) in separate oxygen, and thus provide oxygen stream, described oxygen stream advantageously 100%
Pure oxygen stream.Generally, substantial residual component is nitrogen, especially is used as comprising oxygen when air
In the case of the gas of gas.In order to obtain enough separating resultings, the most necessarily, inoranic membrane 58 is
The finest and close.Compact inorganic film 58 is permeable to oxygen, but (the most right to other gases
Nitrogen) it is strict or the most impervious.
In order to realize these character, inoranic membrane 58 can be solid ceramic film, and it includes selected nothing
Machine oxidation mixture.Preferably inoranic membrane is based primarily upon perovskite or fluorite crystals structure.Such as, calcium titanium
The material Ba that ore deposit is relevant0.5Sr0.5Co0.5Fe0.2O3-δ(BSCF) it is the most suitable.These kinds
The general aspects of inoranic membrane be they be at room temperature all impermeable to described gas, but when be added
Heat and temperature raise time allow oxygen molecule pass.Generally, for the oxygen stream realized, simultaneously
When requiring nothing more than undersized film, the temperature higher than 700K is necessary.Such as, BSCF mentioned above
13ml/cm can be provided at 1275K2The oxygen stream of min, wherein, the film thickness of only 0.2mm is
Enough.
Inoranic membrane can be the transport membrane of the ion-electron of the conveying film of pure oxygen or mixing.Logical
Often, it is necessary to applying power passes through described film making oxygen transmission.This can be electrical force.It is preferable, however, that
Ground, due to the pressure differential between major opposing side and the secondary side of inoranic membrane 58, oxygen passes inoranic membrane 58.
Simultaneously in plasma-pump 16, compression to the gas comprising oxygen result in the master of inoranic membrane 58
Pressure differential between side and secondary side.Due to this effect, generate the oxygen of increase at major opposing side
Edema caused by disorder of QI pressure, it correspondingly makes oxygen stream can stride across inoranic membrane 58 through inoranic membrane 58 or transmission.Also
Can be by providing the pressure instead master at inoranic membrane 58 of reduction on the secondary side of inoranic membrane 58
Face or the pressure increased to there offer extraly make this stream further enhance.Under extreme conditions,
Vacuum can be provided on the secondary side of inoranic membrane 58 to provide the sufficiently high oxygen by described film 58
Air-flow.
In the case of using the pressure of reduction the most on the secondary side, it is preferable that in the upstream of inoranic membrane 58
Use the pressure of >=2.5 bars, on its major opposing side, thus use the pressure of >=2.5 bars.In this article,
Particularly preferably use the pressure in the range of 5 bars or≤5 bars.Rely on inoranic membrane 58 temperature and after
The yardstick of person, can realize the oxygen that appropriateness raises compared with the atmospheric pressure approximating 1 bar at outlet 28
Stream.This can utilize the pressure of the gas comprising oxygen being substantially reduced relative to prior art to realize.
Pressure limit according to the present invention is particularly suitable for home care application.
Obviously, inoranic membrane 58 must be sufficiently stable to meet these conditions as above.This is especially
Important, because preferably forming inoranic membrane 58 with the least size or thickness.Especially, by
The barometric gradient of extension is provided between major opposing side and the secondary side of inoranic membrane 58, inoranic membrane 58 is fixed
It is probably favourable on a support.Supporter can be formed as perforated membrane, especially for coarse mistake
The thick inoranic membrane of filter.Perforated membrane refers in this case to gas permeable choosing non-to oxygen
The film of selecting property.This achieves the stability of enhancing of inoranic membrane 58, it is not necessary to formed the most more stable
Inoranic membrane.This further reduces cost, because stable is film supporter with formation parts, its
More less expensive than inoranic membrane 58.
As described above, it is necessary to heat to obtain enough Oxygen permeability to inoranic membrane 58.
According to the present invention, this is to realize by a kind of easy and simple mode.Due to provide for
The plasma-pump of the gas that compressed package is oxygenous, is heated to sufficiently high temperature by compressed gas simultaneously
Degree scope to be heated to its operation temperature by inoranic membrane 58.Exemplary temperature range is >=700K
Temperature.Particularly preferably the gas comprising oxygen is heated and thus inoranic membrane is heated to >=900K
Scope to≤1300K.In these temperature ranges, it is possible to achieve most suitable oxygen stream.
Therefore, for compression and heating comprise oxygen gas plasma-pump 16 with for from remaining
The combination of the inoranic membrane 58 separating oxygen in the stream being detained improves the energy efficiency of device 10.Need not
The gas comprising oxygen for heating other devices thus heating inoranic membrane are provided.This makes basis
Assembly of the invention 10 reduces cost and further enhancing size and weight properties, and this is for family
It is even more important for nursing application.Additionally, due to the high temperature generated in plasma-pump, comprise oxygen
Gas by asepticization, the most described device is " automatically cleaning " type.This has makes to be generated
The further advantage that oxygen is aseptic, this is preferred for substantial amounts of application.
Referring back to Fig. 1, film unit 22 also includes exporting 68, and it is connected to internal duct 56 in side
And may be coupled to air at opposite side.By exporting 68, the gas that oxygen gas component reduces, especially
Nitrogen, have left film unit 22.This is the discharge gas of film unit 22.If in internal duct 56
The internal pressure that provides, outlet 68 can include another valve 70, and this is especially advantageous.
In the downstream of film unit 22, can include that the pipeline 24 of another valve such as check-valves is connected to
Outlet 28.Outlet 28 can be furnished with mouthpart 72 etc., it is achieved to directly bestowing of the oxygen generated.
It is, therefore, possible to provide be used for obtaining the extra valve of the sufficient stream of pure oxygen or little compressor.?
The downstream of pipeline 24, but in the upstream of outlet 28, can be with optionally provided cooler 26.Can be in order to
Air (using ventilation blower etc.) by surrounding completes the cooling of cooler 26 by forced air stream.
This is probably necessity, because the downstream oxygen at inoranic membrane 58 still has high temperature, and this
It is favourable for making generated oxygen drop to (in the case of exemplary) room temperature for substantial amounts of application.
It may be advantageous, however, that oxygen is not lowered the temperature, because had the oxygen of high temperature by utilization, certain
A little therapies based on oxygen are more effectively.
Although having illustrated and described the present invention, such figure in accompanying drawing and previous explanation in detail
Show and illustrate should to be considered as illustrative or exemplary, and nonrestrictive；The present invention does not limit
In the disclosed embodiments.Those skilled in the art are from the research to accompanying drawing, disclosure and claim
During the present invention required by middle enforcement, it is to be understood that and realize other modification to the disclosed embodiments.
In the claims, " including " word is not excluded for other elements or step, indefinite article " " or " one
Individual " it is not precluded from repetition form.It is true that cited in mutually different dependent claims
Certain measures does not indicates that the combination using these measures that can not be favourable.Any ginseng in claim
Examine labelling to be understood not to scope is construed as limiting.
Claims (13)
1. the method separating oxygen from the gas comprising oxygen, described method comprises the steps:
The gas compressed in plasma-pump (16) and comprise oxygen described in heating,
Heated and compression the gas comprising oxygen is guided the major opposing side to compact inorganic film (58),
Thus
By the described gas comprising oxygen, described inoranic membrane (58) is heated to the permeable temperature of oxygen,
And
Pressure differential is produced, wherein between the described major opposing side and secondary side of described inoranic membrane (58)
Create the oxygen stream by described inoranic membrane (58), thus from the described gas comprising oxygen
Middle separation oxygen.
Method the most according to claim 1, wherein, uses air as the gas comprising oxygen.
Method the most according to claim 1 and 2, wherein, by the described gas pressure comprising oxygen
It is reduced to >=the scope of 2.5 bars, to directly obtain the oxygen pressure of superatmospheric on described side.
Method the most according to claim 3, wherein, arrives the described gas compression comprising oxygen
The scope of 5 bars.
Method the most according to claim 1 and 2, wherein, adds the described gas comprising oxygen
Heat is to >=900K and the temperature range of≤1300K.
Method the most according to claim 1 and 2, wherein, carries out cold to oxygen after releasing
But.
7. an oxygen separation device (10), including:
Plasma-pump (16), it is for compression and heats the gas comprising oxygen, and
Film unit (22), it has compact inorganic film (58), wherein
Described plasma-pump (16) and described film unit (22), described pipe is connected via pipeline (18)
Road is designed to guide heated and compression the gas comprising oxygen from described plasma-pump (16)
To described film unit (22), and
Described compact inorganic film is designed to from the described gas comprising oxygen separate oxygen.
Device the most according to claim 7 (10), wherein, forms described nothing with tubular form
Machine film (58).
9. according to the device (10) described in claim 7 or 8, wherein, described device (10) bag
Include the cooler (26) in the downstream being disposed in described film unit (22).
10. according to the device (10) described in claim 7 or 8, wherein, in described plasma-pump (16)
Downstream provide pneumatic reservoir (52).
11. according to the device (10) described in claim 7 or 8, wherein, described inoranic membrane (58)
It is fixed to be formed as the supporter of perforated membrane.
12., according to the device (10) described in claim 7 or 8, also include inner shell (62),
Between described inoranic membrane (58) and described inner shell (62), wherein limit exterior line (60),
And outside offer the at described inner shell (62) is thermally isolated (64).
13. devices according to claim 12 (10), wherein, described in (64) quilt is thermally isolated
It is designed as vacuum.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP09179682.1 | 2009-12-17 | ||
| EP09179682 | 2009-12-17 | ||
| PCT/IB2010/055787 WO2011073889A1 (en) | 2009-12-17 | 2010-12-14 | Oxygen separation method and system with a plasma pump and a membrane |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102753251A CN102753251A (en) | 2012-10-24 |
| CN102753251B true CN102753251B (en) | 2016-11-16 |
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| CN201080056788.8A Active CN102753251B (en) | 2009-12-17 | 2010-12-14 | Utilize plasma-pump and the oxygen separation method of film and system |
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| US (1) | US8696795B2 (en) |
| EP (1) | EP2512635B1 (en) |
| JP (1) | JP6096513B2 (en) |
| CN (1) | CN102753251B (en) |
| WO (1) | WO2011073889A1 (en) |
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| CA2797101A1 (en) | 2010-08-05 | 2012-02-09 | Hanwha Chemical Corporation | Preparation of extremely small and uniform sized, iron oxide-based paramagnetic or pseudo-paramagnetic nanoparticles and mri t1 contrast agents using the same |
| BR112013006250B1 (en) * | 2010-09-22 | 2021-07-13 | Koninklijke Philips N.V. | METHOD AND DISPOSITION OF GENERATION OF A GAS INCLUDING OXYGEN AND NITRIC OXIDE |
| EP2701825B1 (en) * | 2011-04-28 | 2018-12-12 | Koninklijke Philips N.V. | Method and arrangement for generating oxygen |
| US20150097485A1 (en) * | 2013-10-08 | 2015-04-09 | XEI Scientific Inc. | Method and apparatus for plasma ignition in high vacuum chambers |
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- 2010-12-14 WO PCT/IB2010/055787 patent/WO2011073889A1/en active Application Filing
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|---|---|
| EP2512635A1 (en) | 2012-10-24 |
| JP2013514123A (en) | 2013-04-25 |
| EP2512635B1 (en) | 2016-03-16 |
| WO2011073889A1 (en) | 2011-06-23 |
| US20120247329A1 (en) | 2012-10-04 |
| CN102753251A (en) | 2012-10-24 |
| JP6096513B2 (en) | 2017-03-15 |
| US8696795B2 (en) | 2014-04-15 |
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